FIELD OF THE INVENTION
[0001] This invention relates to a polyester container having enhanced gas barrier properties
as well as to a method of making a polyester container having enhanced gas barrier
properties.
BACKGROUND
[0002] Polyethylene terephthalate and polyethylene terephthalate copolymers (hereinafter
referred to collectively as "PET") are widely used to make containers for carbonated
soft drinks, juice, water, and the like due to their excellent combination of clarity,
mechanical, and gas barrier properties. In spite of these desirable characteristics,
oxygen and carbon dioxide gas barrier properties of PET limit application of PET for
smaller sized packages, as well as for packaging oxygen sensitive products, such as
beer, juice, and tea products. A widely expressed need exists in the packaging industry
to further improve the gas barrier properties of PET.
[0003] The relatively high permeability of PET to carbon dioxide limits the use of smaller
PET containers for packaging carbonated soft drinks. The permeation rate of carbon
dioxide through PET containers is in the range of 3 to 14 cc's per day or 1.5 to 2
percent per week at room temperature depending on the size of the container. A smaller
container has a larger surface area to volume ratio resulting in a higher relative
loss rate. For this reason, PET is currently only used to make larger containers for
packaging carbonated soft drinks, while metal and glass containers are the preferred
materials for making smaller carbonated soft drink containers.
[0004] The amount of carbon dioxide remaining in a packaged carbonated soft drink determines
its shelf life. Normally, carbonated soft drink containers are filled with approximately
four volumes of carbon dioxide per volume of water. It is generally accepted that
a packaged carbonated soft drink reaches the end of its shelf life when 17.5 percent
of the carbon dioxide in the container is lost due to permeation of the carbon dioxide
through the container side wall and closure. The permeability of PET to carbon dioxide
therefore determines the shelf life of the packaged carbonated beverage and thus,
the suitability of PET as a packaging material.
[0005] Numerous technologies have been developed or are being developed to enhance the barrier
of PET to small gas molecules, such as carbon dioxide. For example, the use of a high
barrier layer either as a coating or sandwiched between two layers of PET. The adoption
of a barrier layer adds considerable expense to the manufacturing process, impact
the container's mechanical performance and- in the case of a coating layer- and also
impact the container's appearance.
[0006] Barrier additives eliminate the manufacturing complexity and cost associated with
a separate barrier layer. Yet, many known additives provide only modest barrier improvement
while causing undesirable changes in PET, including the material's mechanical properties,
stretch ratio, and/or clarity.
[0007] U.S. Patent No. 7,820,258 discloses a polyester container with enhanced gas barrier properties. The polyester
container is formed from a polyester composition comprising a polyester and a purine
derivative. In one embodiment, the purine derivative is a purine dione, such as caffeine.
[0008] There remains a need to enhance the barrier performance of polyester containers,
such as PET containers, for use in applications that will require an enhanced barrier,
such as in the packaging of carbonated beverages and oxygen sensitive beverages and
foods, in an economical manner that meets safety, performance and recyclability requirements.
SUMMARY OF THE INVENTION
[0009] The present invention is directed to a polyester container comprising a polyester
composition comprising a polyester and a gas barrier enhancing additive. In an embodiment,
the present invention is a polyester container having enhanced gas barrier properties
comprising a polyester composition comprising a polyester and a gas barrier enhancing
additive, wherein the gas barrier enhancing additive is a compound of Formula I:
wherein i, ii, iii, iv, v, n, n', n", n‴, and m are 0 or 1;
wherein p is an integer from 0 to 50;
wherein Z is a carbon or nitrogen atom;
wherein A, A', A", A‴, and Ae are selected from the group consisting of hydrogen, hydroxyl, primary amine, secondary
amine, and unsubstituted or substituted C1-C20 hydrocarbyl, wherein the C1-C20 hydrocarbyl is mono-, di-, tri-, or tetravalent;
wherein each Y, independent of one another, is a compound having the chemical structure
of Formula II:

wherein t, t1, x, x1, x2, y, and z, independent of one another, are a single bond or a double bond; wherein
t', x', y', and z', independent of one another, are 0 or 1; wherein x", y", and w',
independent of one another, are 0, 1 or 2;
wherein when one or more of ii, iii, iv, and v are 1, A, A' (or Ae), A", and A‴, respectively and independent of one other, is singly or doubly bonded
to atom a, c, or f in structure Y, or singly bonded to atom b, d, e, or g in structure
Y;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom b in structure Y, x' is 0,
and x is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom c in structure Y, y" is 1 and
y is a single bond, or y" is 0 and y is a double bond; wherein when one or more of
A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom c in structure Y, y" is 0 and
y is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom d in structure Y, y' is 0 and
y is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom a in structure Y, x" is 1 and
both x and x1 are single bonds, or x" is 0 and one of x and x1 is a double bond; wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom a in structure Y, x" is 0 and
both x and x1 are single bonds;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom e in structure Y, z' is 0 and
z is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom f in structure Y, w' is 1 and
both z and t are single bonds, or w' is 0 and one of z and t is a double bond; wherein
when one or more of A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom f in structure Y, w' is 0 and
both z and t are single bonds;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom g in structure Y, t' is 0 and
both t and t1 are single bonds;
wherein when x is a double bond, x1 is a single bond; wherein when x1 is a double bond, x and x2 are single bonds; wherein when x2 is a double bond, x1 and t1 are single bonds; wherein when t is a double bond, t1 and z are single bonds; wherein when z is a double bond, t is a single bond; wherein
when t1 is a double bond, t and x2 are single bonds; wherein when x is a double bond, x' is 0; wherein when x or x1 is a double bond, x" is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom a in structure Y; wherein
when y is a double bond, y' is 0 and y" is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom c in structure Y; wherein
when t or t1 is a double bond, t' is 0; wherein when z and t are single bonds, w' is 2 if one
or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom f in structure Y; wherein
when z or t is a double bond, w' is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom f in structure Y; wherein
when z is a double bond, z' is 0; wherein when x, y, or z, independent of one another,
is a single bond and one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atoms b, d, or e, respectively,
in structure Y, x', y', or z', independent of one another, is 1;
wherein R1, R3, R5, and R7, independent of one another, comprise a hydrogen, arylamino, alkoxy, aryloxy, alkenyl,
alkynyl, or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl,
heteroaryl, heterocyclic, or acyl group;
wherein R2, R4, and R6, independent of one another, may be moieties attached by a single or double bond;
wherein when R2, R4, or R6 is a moiety attached by a single bond, R2, R4, and R6, independent of one another, is hydrogen, hydroxyl, amino, amido, alkylamino, arylamino,
alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato, mercapto, imino,
sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl, phosphoryl, phosphino,
thioester, thioether, anhydride, oximno, hydrazino, carbamyl, phosphonic acid, phosphonato,
or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl,
heterocyclic, or acyl group;
wherein when R2, R4, or R6 is a moiety attached by a double bond, R2, R4, or R6, independent of one another, is oxygen, sulfur, CR8R9, SO2, NR10; wherein R8 and R9, independent of one another, is hydrogen, hydroxyl, amino, amido, alkylamino, arylamino,
alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato, mercapto, imino,
sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl, phosphoryl, phosphino,
thioester, thioether, anhydride, oximno, hydrazino, carbamyl, phosphonic acid, phosphonato,
or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl,
heterocyclic, or acyl group; and R10 is hydrogen, arylamino, alkoxy, aryloxy, alkenyl, alkynyl, or a straight, chained,
branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl, heterocyclic, or acyl
group;
wherein when x" is 2, both R4 moieties may be the same or different; wherein when y" is 2, both R2 moieties may be the same or different; and wherein when w' is 2, both R6 moieties may be the same or different, and wherein the gas barrier enhancing additive
is a purine derivative selected from the group consisting of purine dimers, purine
trimers and purine tetramers.
[0010] According to another embodiment, the present invention is a method for making a polyester
container having enhanced gas barrier properties comprising blending a polyester with
a gas barrier enhancing additive as defined above to form a polyester composition
and forming the polyester composition into a container. In one embodiment, the step
of forming the container comprises stretch blow molding.
[0011] In a particular embodiment, the polyester is poly(ethylene terethphalate) based copolymer
(PET copolymer).
[0012] The polyester containers of the present invention exhibit improved properties compared
to conventional polyester containers. In one embodiment, the polyester container of
the present invention exhibits a desirable barrier improvement factor (BIF). In another
embodiment, the polyester container of the present invention exhibits improvement
in shelf-life in comparison to a standard polyester container. In yet another embodiment,
the polyester container of the present invention exhibits improved gas barrier properties
for oxygen, carbon dioxide or both oxygen and carbon dioxide. In still another embodiment,
the polyester container of the present invention exhibits a loss rate reduced by a
factor of 0.95 over a standard polyester bottle. In a further embodiment, the shelf-life
of the polyester container of the present invention is from about 10 weeks to 20 weeks.
[0013] In one particular embodiment, the polyester container of the present invention is
a food or beverage container.
[0014] In a particular embodiment, the polyester container is a carbonated soft drink container,
an oxygen-sensitive beverage container or an oxygen-sensitive food container.
[0015] Particular embodiments may achieve this enhanced gas barrier while offering safety,
performance and recyclability.
[0016] Other objects, features, and advantages of this invention will become apparent from
the following detailed description, drawings, and claims.
BRIEF DESCRIPTON OF THE DRAWINGS
[0017]
Fig. 1 is a schematic diagram of a system for making a polyester container such as a PET
container with enhanced gas barrier in accordance with an embodiment of the present
invention.
Fig. 2 is a sectional elevation view of a molded container preform made in accordance with
an embodiment of the present invention.
Fig. 3 is a sectional elevation view of a blow molded container made from the preform of
Fig. 2 in accordance with an embodiment of the present invention.
Fig. 4 is a perspective view of a packaged beverage made in accordance with an embodiment
of the present invention.
Fig. 5 shows mass loss curves of PET bottle resin (1101) at temperatures of 120 to 180 °C.
Fig. 6 shows mass loss curves of XCP-3 at temperatures of 120 to 180 °C.
Fig. 7 shows mass loss curves at 180 °C. The 95% prediction interval shows an indication
of the range in which the data could represent the vapor pressure for PET resin. This
data indicates ±0.008 mg/min, which translates to ± 15 Pa at 180 °C. It is therefore
reasonable to assume that 15 Pa would be a cutoff for reliability of PET resin.
DETAILED DESCRIPTION
[0018] This invention relates to a polyester container comprising a polyester composition
comprising a polyester and a gas barrier enhancing additive as defined above and to
methods for making such containers. These are further described below and in the accompanying
figures.
I. Polyester
[0019] The polyester may be any suitable polyester. The polyester may be a homopolymer or
a copolymer, partially or wholly derived from petrochemicals or partially or wholly
derived from biomass. In a particular embodiment, the polyester is suitable for use
in the manufacture of containers. Suitable polyesters for use in the present invention
include, but are not limited to, polyethylene terephthalate (PET), PET copolymers,
PET blends, polyethylene naphthalate (PEN), polyethylene isophthalate, nylons, aliphatic
polyesters (e.g. poly(hydroxyalkanoic acids and poly(lactic acid)) and the like.
[0020] In a particular embodiment, the polyester is PET. PET comprises a diol component
having repeat units of ethylene glycol and a diacid component having repeat units
of terephthalic acid. PET is commonly used for many applications where a barrier is
desirable, such as films and containers. In particular, PET containers are widely
used for packaging beverages including carbonated soft drinks.
[0021] In another particular embodiment, the polyester is a PET copolymer. PET copolymers
comprise repeating units of ethylene glycol and terephthalic acid, as above, in addition
to another monomer. Like PET, PET copolymers are commonly used for many applications
where a barrier is desirable, such as films and containers. In particular, PET copolymer
containers are widely used for packaging beverages including carbonated soft drinks.
[0022] In a particular embodiment, the present invention is a polyester container comprising
a polyester composition comprising a polyester and a gas barrier enhancing additive,
as described further below. Without being bound by any particular theory, it is believed
that the gas barrier enhancing additive is truly solubilized in PET.
[0023] The weight percentage of the gas barrier enhancing additive relative to the polyester
composition is referred to as the loading level. In a specific embodiment, the loading
level of the gas barrier enhancing additive is desirably in the range of about 0.1
to about 40 weight percent of the polyester composition, such as, for example, from
about 1 to about 10 weight percent, from about 1 to about 5 weight percent, from about
2 to about 5 weight percent or from about 2 to about 3 weight percent. In a particular
embodiment, the gas barrier enhancing additive is about 2 weight percent of the polyester
composition. In a particular embodiment, the gas barrier additive is about 3 weight
percent of the polyester composition.
[0024] According to one embodiment, the polyester container comprising the polyester composition
comprises: a) a polyester, wherein the polyester is present in an amount in the range
of about 60 to about 99.8 weight percent of the polyester composition; and b) a gas
barrier enhancing additive, wherein the gas barrier enhancing additive is present
in an amount in the range of about 0.2 to about 40 weight percent of the polyester
composition. In a particular embodiment, the polyester is a PET copolymer.
[0025] According to one embodiment, the polyester is present in in an amount in the range
of about 70 to about 99.8 weight percent of the polyester composition, about 80 to
about 99.8 weight percent of the polyester composition or about 90 to about 99.8 weight
percent of the polyester composition.
[0026] In a particular embodiment, the polyester container comprises a polyester composition
which comprises: a) a polyester, wherein the polyester is present in an amount in
the range of about 90 to about 99.8 weight percent of the polyester composition; and
b) a gas barrier enhancing additive, wherein the gas barrier enhancing additive is
in an amount in the range of about 0.2 to about 10 weight percent of the polyester
composition. In some embodiments, the polyester composition comprises a polyester
in an amount in the range of about 90 to about 99.8 weight percent and the remainder
of the polyester composition comprises the gas barrier enhancing additive.
II. Gas Barrier Enhancing Additive
[0027] In one embodiment, the present invention is a polyester composition comprising a
polyester and a gas permeation enhancing additive, wherein the gas barrier enhancing
additive is a compound of Formula I as defined above and which is a purine derivative
selected from the group consisting of purine dimers, purine trimers and purine tetramers..
The compound of Formula I provides at least the following characteristics: (1) lower
volatility; (2) decreased rate of migration of from the packaging into the product;
and 3) multiple interactions that may offset some of the additional plasticization
effects.
[0028] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
34:
wherein x' and y', independent of one another, are 0 or 1;
wherein x", y", and w', independent of one another, are 0, 1 or 2;
wherein R1 and R3, independent of one another, comprise a hydrogen, arylamino, alkoxy, aryloxy, alkenyl,
alkynyl, or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl,
heteroaryl, heterocyclic, or acyl group;
wherein R2 and R4, independent of one another, may be moieties attached by a single or double bond;
wherein when R2 or R4 is a moiety attached by a single bond, R2 and R4, independent of one another, is hydrogen, hydroxyl, amino, amido, alkylamino, arylamino,
alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato, mercapto, imino,
sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl, phosphoryl, phosphino,
thioester, thioether, anhydride, oximno, hydrazino, carbamyl, phosphonic acid, phosphonato,
or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl,
heterocyclic, or acyl group;
wherein when R2 or R4 is a moiety attached by a double bond, R2 or R4, independent of one another, is oxygen, sulfur, CR8R9, SO2, NR10; wherein R8 and R9, independent of one another, is hydrogen, hydroxyl, amino, amido, alkylamino, arylamino,
alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato, mercapto, imino,
sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl, phosphoryl, phosphino,
thioester, thioether, anhydride, oximno, hydrazino, carbamyl, phosphonic acid, phosphonato,
or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl,
heterocyclic, or acyl group; and R10 is hydrogen, arylamino, alkoxy, aryloxy, alkenyl, alkynyl, or a straight, chained,
branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl, heterocyclic, or acyl
group; and
wherein R6 is a moiety attached by a single bond and R6 is hydrogen, hydroxyl, amino, amido, alkylamino, arylamino, alkoxy, aryloxy, nitro,
acyl, alkenyl, alkynyl, cyano, sulfo, sulfato, mercapto, imino, sulfonyl, sulfenyl,
sulfinyl, sulfamoyl, phosphonyl, phosphinyl, phosphoryl, phosphino, thioester, thioether,
anhydride, oximno, hydrazino, carbamyl, phosphonic acid, phosphonato, or a straight,
chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl, heterocyclic,
or acyl group.
[0029] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
34, wherein x' and y' in each purine nucleus (structure Y) are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ia
52:

[0030] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
34, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ia
35:

[0031] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
35, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls,
i.e. methyl groups. In this embodiment, the gas barrier enhancing additive has the chemical
structure of Formula Ia
36:

[0032] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
36, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of XCP-1:

[0033] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
7:

wherein z' is 0 or 1; and
wherein R
5 comprises a hydrogen, arylamino, alkoxy, aryloxy, alkenyl, alkynyl, or a straight,
chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl, heterocyclic,
or acyl group.
[0034] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
7, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
53:

[0035] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
7, wherein y" and x" are 1 in each structure Y, and R
2 and R
4, in each structure Y, are oxygen atoms doubly bonded to atoms c and a, respectively,
in each structure Y. In this embodiment, the compound has the chemical structure of
Formula Ia
8:

[0036] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
8, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
9:

[0037] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
9, wherein w' is 1 in each structure Y, and R
6 is a hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of XCP-2:

[0038] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
41:

[0039] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
41, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ia
54:

[0040] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
41, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ia
42:

[0041] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
42, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ia
43:

[0042] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
43, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of XCP-3:

[0043] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
17:

[0044] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
17, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
55:

[0045] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
17, wherein y" and x" are 1 in each structure Y, and R
2 and R
4, in each structure Y, are oxygen atoms doubly bonded to atoms c and a, respectively,
in each structure Y. In this embodiment, the compound has the chemical structure of
Formula Ia
18:

[0046] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
18, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
19:

[0047] In one embodiment, the purine derivative is a compound having the chemical structure
of Formula Ia
19, wherein w' is 1 in each structure Y, and R
6 is a hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of XCP-5:

[0048] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
48:

[0049] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
48, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ia
56:

[0050] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
48, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ia
49:

[0051] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
49, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ia
50:

[0052] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
50, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
51:

[0053] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ia
27:

[0054] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
27, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
57:

[0055] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
27, wherein y" and x" are 1 in each structure Y, and R
2 and R
4, in each structure Y, are oxygen atoms doubly bonded to atoms c and a, respectively,
in each structure Y. In this embodiment, the compound has the chemical structure of
Formula Ia
28:

[0056] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
28, wherein z' and y' are 1 in each structure Y, and R
3 and R
5 are C
1 alkyls,
i.e. methyl groups, in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
29:

[0057] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ia
29, wherein w' is 1 in each structure Y, and R
6 is a hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ia
30:

[0059] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ib
9:

[0060] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
9, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls,
i.e. methyl groups. In this embodiment, the compound has the chemical structure of Formula
Ib
10:

[0061] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
10, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ib
11:

[0062] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
11, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ib
12:

[0063] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
12, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ib
13:

[0064] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ib
16:

[0065] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
16, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ib
17:

[0066] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
17, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ib
18:

[0067] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
18, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ib
19:

[0068] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
19, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ib
20:

[0069] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ib
28:

[0070] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
27, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ib
29:

[0071] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
29, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ib
30:

[0072] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
30, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ib
31:

[0073] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ib
34:

[0074] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
34, wherein z' and y' in each structure Y are 1, and R
5 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ib
35:

[0075] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
35, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ib
36:

[0076] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
36, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls,
i.e. methyl groups. In this embodiment, the compound has the chemical structure of Formula
Ib
37:

[0077] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ib
37, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ib
38:

[0078] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ic
7:

[0079] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
7, wherein z' and y' in each structure Y are 1, and R
5 and R
3 are C
1 alkyls,
i.e. methyl groups. In this embodiment, the compound has the chemical structure of Formula
Ic
8:

[0080] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
7, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ic
9:

[0081] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
9, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls,
i.e. methyl groups. In this embodiment, the compound has the chemical structure of Formula
Ic
10:

[0082] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
10, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ic
11:

[0083] In one embodiment, the gas barrier enhancing additive has the chemical structure
of Formula Ic
13:

[0084] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
13, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ic
14:

[0085] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
13, wherein x" and y" in each structure Y are 1, and R
2 and R
4 are, in each structure Y, oxygen atoms that are doubly bonded to atoms c and a, respectively.
In this embodiment, the compound has the chemical structure of Formula Ic
15:

[0086] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
15, wherein x' and y' in each structure Y are 1, and R
1 and R
3 are C
1 alkyls, i.e. methyl groups. In this embodiment, the compound has the chemical structure
of Formula Ic
16:

[0087] In one embodiment, the gas barrier enhancing additive is a compound having the chemical
structure of Formula Ic
16, wherein w' is 1 in each structure Y, and R
6 is hydrogen in each structure Y. In this embodiment, the compound has the chemical
structure of Formula Ic
17:

[0088] In another embodiment, the gas barrier enhancing additive has a molecular weight
greater than caffeine, i.e., greater than about 194 g/mole. In a particular embodiment,
the gas barrier enhancing additive has a molecular weight of from about 385 to about
1000 g/mol. In a specific embodiment, the gas barrier enhancing additive has a molecular
weight of from about 400 to about 490 g/mol, from about 410 to about 480 g/mol, from
about 420 to about 470 g/mol, from about 430 to about 460 g/mol or from about 440
to about 450 g/mol.
[0089] In a specific embodiment, the gas barrier additive is a purine dimer, e.g., a caffeine
dimer. In another specific embodiment, the polyester composition of the present invention
comprises a purine trimer, e.g., a caffeine trimer. In a still further specific embodiment,
the gas barrier additive is a purine tetramer, e.g., a caffeine tetramer.
[0090] The gas barrier enhancing additives of the present invention may be synthesized by
any suitable method. Examples 1 and 2 provide representative but non-limiting synthetic
routes to purine derivatives of the present invention.
[0091] In one embodiment, the gas barrier enhancing additive exhibits low volatility. In
a specific embodiment, the gas barrier enhancing additive is less volatile than caffeine.
The volatility of caffeine can make processing a challenge (sublimation point of 178
°C, melting point of 238 °C) since rapid volatilization may produce plate-out on tools,
increase occupational exposure, and make for an unacceptable level of migration in
finished bottles. Polyester compositions containing caffeine are plasticizers from
a mechanical property perspective. Polyester compositions containing caffeine may
also influence the uptake and saturation level of moisture in the composition, which
also contributes to the plasticization effect responsible for the creep observed.
[0092] Volatility of solids can be measured as the vapor pressure of the solid at a temperature
of interest. Vapor pressure can be determined by thermogravimetric analysis (TGA).
Under specific pressure and temperature conditions, the rate of mass loss is directly
proportional the vapor pressure of the solid, provided that the material is truly
isolated in the vapor phase and does not undergo any association or interactions.
If the vapor is continually moved or flushed in a manner such that the vapor never
reaches saturation, then the material will sublime until it has completely vaporized.
The same conditions will be present in the case where a temperature differential exists
such that the material will sublime and then immediately condense back to a solid
at a significantly cooler location. The key is to ensure that the vapor does not reach
a saturation level. The basic equation for the relation of mass loss from TGA to vapor
pressure is a modified Langmuir equation:

[0093] Where M is the molar mass of the subliming molecule, R is the ideal gas constant,
T is the absolute temperature, p is the vapor pressure and α is the vaporization coefficient
(usually assumed to be 1 for tests done in vacuum). If a vacuum is not used, then
the value of α must be determined (it will be non-unity, though stay constant for
the particular instrument and gas flow conditions). Thus, it becomes difficult to
determine both p and α from a single set of experiments unless we can simplify the
definitions and relate them to either known quantities or easily measured quantities.
[0094] Caffeine provides a calibration curve for a specific instrument within a known temperature
range according to the following:

Where P is the partial pressure caffeine and a and b are constants that describe
the instrument. Therefore, a simple plot of the slope of the mass loss at some constant
temperature can be used to give the vapor pressure of any compound. For calibration
purposes, data on the vapor pressure of caffeine can be found in a review by
Emel'yaneko J. Chem. Thermodynamics, 40, 2008, pg. 1661-1665. Example 3 provides a procedure for calculation of the instrument constants.
[0095] To determine the vapor pressure of a solid, a temperature profile similar to that
used above, with the temperature values chosen to be within the range of interest.
It is important that separate experiments be run below and above the melting point
as the interpretation of the data can be complicated by the fact that enthalpies of
sublimation and vaporization have different values.
[0096] Once the vapor pressure as a function of temperature has been determined, comparison
against known materials can provide insight into the propensity of an additive to
plate out onto tools during processing. Additionally, we can determine the enthalpy
of vaporization or sublimation using the Clasius-Claperon equation:

[0097] For temperatures above the melting point, the ΔH
vap is determined; the ΔH
sublimation is determined for temperatures below the melting point. A plot of the In p versus
1/T will yield a slope equal to -ΔH/R and an intercept equal to the Clasius constant,
B. The value of R will determine the units for ΔH. Furthermore, it is important to
use absolute temperatures (Kelvin) in this analysis.
[0098] A comparison of the enthalpies of pure compounds versus compounds in PET matrices
permits evaluation of the effect of compounding of the material, as well as the effects
on equilibrium concentrations and diffusion rates.
[0099] Examples 4 and 5 provide data on the volatility of various gas barrier enhancing
additives disclosed herein.
[0100] In one embodiment, the vapor pressure of the gas barrier enhancing additive at 260
°C is lower than the vapor pressure of caffeine. At 160°C, the vapor pressure of caffeine
is about 36 Pa, for example. In a specific embodiment, the vapor pressure of the additive
at 260 °C is less than about 25 Pa, less than about 20 Pa, less than about 15 Pa,
less than about 10 Pa, less than about 5 Pa, less than about 1 Pa or about zero (o)
Pa. In a preferred embodiment, the vapor pressure of the additive is 0 Pa, i.e., it
is not volatile.
III. Containers
[0101] The polyester compositions described herein are used to form polyester containers
which form part of the invention. Suitable containers include, but are not limited
to, bottles, drums, carafes, coolers, and the like. In one embodiment, the polyester
container is used to store a food or beverage. In a specific embodiment, the polyester
container is used to store a carbonated beverage such as a carbonated soft drink.
[0102] As is well known to those skilled in the art, containers can be made by blow molding
a container preform. Examples of suitable preform and container structures are disclosed
in
U.S. Pat. No. 5,888,598.
[0103] A polyester container preform 12 is illustrated in FIG. 2. This preform 12 is made
by injection molding PET based resin and comprises a threaded neck finish 112 which
terminates at its tower end in a capping flange 114. Below the capping flange 114,
there is a generally cylindrical section 116 which terminates in a section 118 of
gradually increasing external diameter so as to provide for an increasing wall thickness.
Below the section 118 there is an elongated body section 120.
[0104] The preform 12 illustrated in FIG. 2 can be stretch blow molded to form a container
14 illustrated in FIGS. 3 and 4. The container 14 comprises a shell 124 comprising
a threaded neck finish 126 defining a mouth 128, a capping flange 130 below the threaded
neck finish, a tapered section 132 extending from the capping flange, a body section
134 extending below the tapered section, and a base 136 at the bottom of the container.
The container 14 is suitably used to make a packaged beverage 138, as illustrated
in FIG. 4. The packaged beverage 138 includes a beverage such as a carbonated soda
beverage disposed in the container 14 and a closure 140 sealing the mouth 128 of the
container.
[0105] The polyester container optionally may comprise a plurality of layers as described
in co-pending patent application Ser. No.
11/850,575 filed on Sep. 15, 2006, entitled "Multilayer Container having Small Molecule Barrier Additives,". A multilayer
container can permit the use of additives in a barrier layer that normally would be
too volatile for inclusion in a single layer container because the low molecular weight
additive is contained within two outer layers without the low molecular weight additive,
preventing contact between the low molecular weight additive and the surfaces of the
injection molding apparatus.
[0106] Briefly described, a multilayer container comprises at least two outer layers comprising
a polymer matrix and at least one barrier layer disposed between the at least two
outer layers. The at least one barrier layer comprises a polyester composition comprising
a polyester and a gas barrier enhancing additive. as defined above Desirably, the
gas barrier enhancing additive is present in the multilayer container in an amount
in the range of about 0.2 to about 10 weight percent of the container, the at least
two outer layers comprise about 99 to about 20 weight percent of the container, and
the one or more barrier layers comprise about 1 to about 80 weight percent of the
container. In another particular embodiment, the multilayer container further comprises
at least one intermediate layer between the at least one barrier layer and the at
least two outer layers.
[0107] The preform 12, container 14, and packaged beverage 138 are examples of applications
using the preforms of the present invention. It should be understood that the process
and apparatus of the present invention can be used to make preforms and containers
having a variety of configurations.
[0108] In one embodiment, the polyester container of the present invention exhibits a desirable
barrier improvement factor (BIF). The BIF is a measure of enhanced gas barrier properties
(the ratio of the gas transmission rate of a polyester composition without an additive
to the gas transmission rate of a polyester composition with an additive). In one
embodiment, the polyester container exhibits a desirable BIF for oxygen ingress. In
another embodiment, the polyester container exhibits a desirable BIF for carbonation
retention.
[0109] In one embodiment, the BIF of the polyester container of the present invention is
from about 1.0x to about 2.0x increased over a standard polyester container of the
same wall thickness. In a specific embodiment, the BIF of the polyester container
is about 1.1x, about 1.2x, about 1.3x, about 1.4x, about 1.5x, about 1.6x, about 1.7x,
about 1.8x or about 1.9x increased over a standard polyester container of the same
wall thickness.
[0110] In another embodiment, the polyester container of the present invention exhibits
improvement in shelf-life in comparison to a standard polyester container. In one
embodiment, the shelf life of the polyester container of the present invention is
increased from about 1.0x to about 2.0× relative to a standard polyester container.
In a specific embodiment, the shelf-life of the polyester container is about 1.1×,
about 1.2x, about 1.3x, about 1.4x, about 1.5x, about 1.6x, about 1.7x, about 1.8x,
or about 1.9x increased over a standard polyester container.
[0111] In a particular embodiment, the polyester container of the present invention exhibits
improved gas barrier properties for oxygen, carbon dioxide or both oxygen and carbon
dioxide. In one embodiment, oxygen permeation is reduced by about 10%, about 20%,
about 30%, about 40%, about 50%, about 60%, about 70%, about 80 over a standard polyester
container. In another embodiment, carbon dioxide permeation is reduced by a factor
of about 10%, about 20%, about 30%, about 40%, about 50%, about 60%, about 70%, about
80% over a standard polyester container.
[0112] In another particular embodiment, the polyester container of the present invention
exhibits a loss rate reduced by a factor of 0.95 over a standard polyester bottle,
where loss rate is expressed as a % per week, such as, for example, about 0.90, about
0.85, about 0.80, about 0.75, about 0.70, about 0.65, about 0.60, about 0.55, about
0.50, about 0.45, about 0.40, about 0.35, about 0.30 or about 0.25.
[0113] In one embodiment, the shelf-life of the polyester container of the present invention
is from about 10 weeks to about 20 weeks, about 11 weeks to about 19 weeks, about
12 weeks to about 18 weeks, about 13 weeks to about 17 weeks, about 14 weeks to about
16 weeks or about 15 weeks.
[0114] In a further embodiment, the purine derivative exhibits no noticeable effect on the
high pressure creep of the polyester container of the present invention. In a particular
embodiment, the natural stretch ratio (NSR) is similar to that of standard polyester
container.
IV. Methods of Making Polyester Composition and Containers
[0115] As described above, the polyester compositions described herein are useful for making
containers in which enhanced gas barrier is desirable. In short, such containers are
made by forming the above described polyester compositions into the desired container
by conventional methods.
[0116] The polyester is amenable to melt forming processes including, but are not limited
to, injection molding, extrusion, thermal forming and compression molding. Injection
molding describes a process whereby the polyester resin is heated to a temperature
above its glass transition temperature and becomes molten. The molten polyester material
is then injected into a mold. The molten polyester material fills the mold before
cooling. The mold is then opened and the plastic article is released.
[0117] Methods for incorporating the gas barrier enhancing additive into the polyester composition
are well known to those skilled in the art. For example, an additive can be fed directly
into the polyester during the melt forming process, pre-blended with the polyester
resin prior to melting forming, or incorporated at high concentrations with a polyester
as masterbatch and then blended with the polyester resin prior to the melt forming
process container.
[0118] Blow molding may be used to form hollow plastic containers. There are three general
types of blow molding: extrusion blow molding, injection blow molding, and stretch
blow molding. The particularly preferred method for making the containers of this
invention is stretch blow molding.
[0119] FIG. 1 illustrates a system 10 in accordance with an embodiment of this invention
for making a rigid container preform 12 (illustrated in FIG. 2) and a rigid container
14 (illustrated in FIG. 3) from the preform. As is shown in FIG. 1, PET 20 and a gas
barrier enhancing additive 22 are added to a feeder or hopper 24 that delivers the
components to a hot melt extruder 26 in which the components are melted and blended.
The hot melt extruder 26 then extrudes the molten mixture of PET 20 and gas barrier
enhancing additive 22 into an injection molding device 28 to form the preform 12.
The preform 12 is cooled and removed from the injection molding device 28 and delivered
to a stretch blow molding device 30 which stretch blow molds the preform 12 into a
finished rigid container 14.
[0120] The melt residence time of the preform production is preferably less than five minutes
and more preferably from about one to about three minutes. The melt temperatures are
desirably from about 270 to about 300°C and more desirably from about 270 to about
290° C. The melt residence time begins when the PET 20 and gas barrier enhancing additive
22 enter the melt extruder 26 and start melting, and ends after injection of the molten
blend into the injection mold to form the preform 12.
[0121] In a particular embodiment, the injection molding process can be modified by pressurizing
the mold cavity to minimize plate-out, as described in the co-pending U.S. patent
application entitled "Pressurized Tooling for Injection Molding and Method of Using,",
and was filed on Sep. 15, 2006, by Schultheis, et al. Pressurizing the mold cavity
changes the dynamics of the processing cycle by reducing or completely eliminating
the ability of additives to diffuse through the PET copolymer and deposit on the inner
surface of the mold. The desired pressure of the mold cavity can be optimized for
a particular polymer material, polymer matrix, or additive.
[0122] The modified injection molding process (not pictured) includes the additional step
of pressurizing a mold by introducing a pressurized gas into a mold cavity in the
mold, wherein the mold cavity defines the shape of the container preform; introducing
a polyester composition into the mold cavity; cooling the polyester composition to
form the container preform; and removing the container preform from the mold cavity.
[0123] The pressurized gas may be any gas that does not detrimentally affect the polyester
composition. Non-limiting examples include air and its individual components, oxygen,
nitrogen, and carbon dioxide; the noble gases, argon, neon, helium, and xenon; and
mixtures thereof. In a particular embodiment, the mold cavity is pressurized to a
pressure in the range of about 1 to about 1000 psig.
[0124] In one embodiment, the present invention is a method of forming a hollow plastic
container comprising:
(i) providing a polyester resin material;
(ii) heating the polyester resin material to provide a molten resin;
(iii) adding a gas barrier enhancing additive as defined in the appended claim 1 to
the molten resin;
(iv) introducing the molten resin into a mold;
(v) cooling the molten resin to form a preform;
(vi) removing the perform from the mold; and
(vi) blow molding the perform to form a hollow plastic container.
[0125] In another embodiment, the present invention is a method of forming a hollow plastic
container comprising:
(i) providing a polyester resin material comprising a polyester and a gas barrier
enhancing additive, wherein the gas barrier enhancing additive is as defined in the
appended claim 1;
(ii) heating the polyester resin material to provide a molten resin;
(iii) introducing the molten resin into a mold;
(iv) cooling the molten resin to form a preform;
(v) removing the perform from the mold; and
(v) blow molding the perform to form a hollow plastic container.
[0126] In a particular embodiment, the polyester is PET or a PET copolymer.
[0127] In a more particular embodiment, the loading of the gas barrier enhancing additive
is from 2% to about 5%, such as, for example, about 2%, about 3%, about 4% or about
5%. In a preferred embodiment, XCP-3 loading in a preform or bottle is about 3%.
[0128] In a particular embodiment, the container is a PET bottle. In another particular
embodiment, the container is a PET copolymer bottle.
EXAMPLES
Example 1 General Preparation of (Alkanediyl)bis[theophylline]
[0129] A 1 mmol/10 mL concentration solution of theophylline in anhydrous dimethylformamide
(DMF) was prepared under an inert gas atmosphere and dry conditions. For one equivalent
of theophylline, an equimolar amount of sodium hydride was carefully added to the
solution, followed by one half an equivalent of dibromoalkane. The dibromoalkanes
included dibromopropane, dibromobutane, and dibromooctane.
[0130] The mixture was stirred at ambient temperature (∼ 22 °C) for 15 hours, then heated
and stirred at 70 °C for three hours. The progress of the reactions was monitored
using thin-layer chromatography (TLC), by confirming the consumption of the starting
materials. The resulting mixture was poured into water to produce a solid mass of
the product compound. The product was further purified by column chromatography, which
yielded a pure, white, amorphous compound.
Example 2 Preparation of MU2951-12
[0131] Formula C
16H
18N
8O
4, molecular weight: 386.4, Standard name: 7-[4-(1,3-dimethyl-2,6-dioxide-2,3,6,7-4H-1H-purine-7-yl)ethyl]-1,3-dimethyl-2,3,6,7-4H-1H-purine
-2,6-dione:

[0132] Procedure 1: 72 g theophylline (400 mmol), 0.16 g KI and 360 ml pure water were added sequentially
to a 1000 ml four mouth flask. The mixture was stirred and heated to 50°C and incubated
for 60 minutes. The pH of the mixture was then adjusted to 14 with a 30% liquid alkaline.
After pH 14 was reached, the mixture was heated to 60°C. 19.8 g (200mmol) of 1,2-dichloroethane
was then added dropwise over a period of 3 hours and the mixture was incubated for
48 hours. The mixture was then filtered, washed with water and vacuum filtered to
provide MU2951-12 (46.7 g dry weight, 60.4% yield).
[0133] Procedure 2: 72 g theophylline (400 mmol), 2.0 g KI and 500 ml DMF were added sequentially to
a 1000 ml four mouth flask. The mixture was stirred and heated to 85°C and incubated
for 40 minutes. 34.6 g K
2CO
3 (250mmol) was added. The mixture was heated to 98°C, then 37.6 g (200mmol) of 1,2-dibromoethane
was added dropwise over 0.5 hours and the mixture was incubated for 10 hours. The
mixture was then filtered, washed with water and filtered to provide MU2951-12 (48.9
g dry weight, 63.3% yield).
Example 3: Preparation of Compound 2
[0134] Formula C
17H
20N
8O
4, molecular weight: 400.4, Standard name: 7-[4-(1,3-dimethyl-2,6-dioxide-2,3,6,7-4H-1H-purine-7-yl)propyl]1,3-dimethyl-2,3,6,7-4H-1H-purine
-2,6-dione

[0135] Procedure 1: 72 g theophylline (400 mmol) , 0.16 g KI and 400 ml pure water were added sequentially
to a 1000 ml four mouth flask. The mixture was stirred and heated to 50°C and incubated
for 60 minutes. The pH of the mixture was adjusted to 12 with a 30% liquid alkaline.
Once the pH was adjusted, the mixture was heated to 60°C. 22.6 g (200mmol) of 1,3-dichloropropane
was added in one portion and the mixture was incubated for 48 hour at 60°C. The mixture
was filtered, washed with water and filtrated to provide Compound 2 (50.9 g, dry weight
50.9 g, 63.6% yield).
[0136] Procedure 2: 72 g theophylline (400 mmol), 2.0 g KI and 900 ml DMF were added sequentially to
a 2000 ml four mouth flask. The mixture was stirred and heated to 85°C and incubated
for 40 minutes. 69.1g K
2CO
3 (500mmol) was then added. The mixture was heated to 98°C, then 80.8 g (400mmol) of
1,3-dibromopropane was added dropwise over 0.5 hours. The mixture was then incubated
for 10 hours. The mixture was filtered, washed with water and filtrated to provide
Compound 2 (54.2 g dry weight, 67.7% yield).
Example 4: Preparation of XCP-3
[0137] C
18H
22N
8O
4 Formula C
18H
22N
8O
4, molecular weight: 414.4, Standard name:7-[4-(1,3-dimethyl-2,6-dioxide-2,3,6,7-4H-1H-purine-7-yl)butyl]-1,3-dimethyl-2,3,6,7-4H-1H-purine
-2,6-dione

[0138] Procedure 1: 36 g theophylline (200 mmol), 1.6 g KI and 720 ml pure water were added seqeuntially
to a 1000 ml four mouth flask. The mixture was stirred and heated to 70°C and incubated
for 60 minutes. The pH of the mixture was adjusted to pH 9 with a 30% liquid alkaline
(30% sodium hydroxide in water). The mixture was then heated to 90°C, and 43.2 g (200mmol)
of 1,4-dibromobutane was added dropwise over 4 hours. The mixture was incubated for
36 hours at 90°C. The mixture was filtered, washed with water and filtrated to provide
XCP-3 (33.2 g dry weight, 80.1% yield).
[0139] Procedure 2: 36 g theophylline (200 mmol), 0.3g KI and 450ml DMF were added sequentially to a
1000 ml four mouth flask. The mixture was stirred and heated to 85°C and incubated
for 40 minutes. 20.7g K
2CO
3 (150mmol) was then added. The mixture was heated to 98 °C, then 12.7 g (100mmol)
1,4-dichlorobutane was added at once and incubated for 4 hours. The mixture was filtered,
washed with water and filtrated to provide XCP-3, (34.1 g dry weight, 82.3% yield).
Example 5: Preparation of MU2951-11
[0140] Formula C
19H
24N
8O
4, molecular weight 428.4., Standard name: 7-[4-(1,3-dimethyl-2,6-dioxide-2,3,6,7-4H-1H-purine-7-yl)amyl]-1,3-dimethyl-2,3,6,7-4H-1H-purine
-2,6-dione

[0141] Procedure 1: 36 g theophylline (200 mmol), 1.6 g KI and 720 ml pure water were added sequentially
to a 1000 ml four mouth flask. The mixture was stirred, heated to 70°C and incubated
for 60 minutes. The pH of the mixture was adjusted to pH 10 with a 30% liquid alkaline
(30% sodium hydroxide in water). After achieving pH 10, the mixture was heated to
90°C, and 46.0 g (200mmol) of 1,5-dibromopentane was added dropwise over 1 hour. The
mixture was then incubated for 36 hours for pH 9~10. Then it was filtered, washed
with water and filtrated to provide MU2951-11 (36.0 g dry weight, 84.0% yield).
[0142] Procedure 2: 36 g theophylline (200 mmol), 0.3g KI and 450ml DMF were added sequentially
to a 1000 ml four mouth flask. The mixture was stirred and heated to 85°C and incubated
for 40 minutes. 20.7g K
2CO
3 (150mmol) was then added. The mixture was heated to 98°C and 14.1 g (100mmol) of
1,5- dichloropentane was added dropwise over 0.5 hours. The mixture was incubated
for 4 hours, then filtered, washed with water and filtrated to provide MU2951-11 (35.8
g dry weight, 83.6% yield).
Example 6: Preparation of XCP-4
[0143] Formula C
20H
26N
8O
4, molecular weight 442.4, Standard name: 7-[4-(1,3-dimethyl-2,6-dioxide-2,3,6,7-4H-1H-purine-7-yl)hexyl]-1,3-iimethyl-2,3,6,7-4H-1H-purine
-2,6-dione

[0144] Procedure 1: 108 g theophylline (600 mmol), 3.0 g KI and 1000 ml pure water were added sequentially
to a 2000 ml four mouth flask. The mixture was stirred and heated to 50°C and incubated
for 10 minutes. The pH of the mixture was adjusted to 10 with a 30% liquid alkaline.
Once a pH of 10 was obtained, the mixture was heated to 60°C. 117.1 g (480mmol) of
1,6-dibromohexane was added at once, and the mixture was incubated for 4 hours for
pH 10. The mixture was filtered, washed with water and filtrated to provide XCP-4
(104.6 g dry weight, 78.9% yield).
[0145] Procedure 2: 108g theophylline (600 mmol), 0.2g KI, and 500ml DMF were added sequentially to a
1000 ml four mouth flask. The mixture was stirred and heated to 60°C and incubated
for 20 minutes. 20.7g K
2CO
3 (150mmol) was added and the mixture was heated to 80°C. 18.6 g (120mmol) of 1,6-dichlorohexane
was then added dropwise over 5 hours. The mixture was incubated for 36 hours. Then
mixture was then filtered, washed with water and filtrated to provide XCP-4 (39.6g
dry weight, 74.6% yield).
Example 7 - General Preparation of (Alkanediyl)bis[theobromine]
[0146] A 1 mmol/10 mL concentration solution of theobromine in anhydrous DMF was prepared
under an inert gas atmosphere in dry conditions. For one equivalent of theobromine,
an equimolar amount of sodium hydride was carefully added, followed by one half an
equivalent of dibromoalkane. The dibromoalkanes included dibromopropane, dibromobutane,
and dibromooctane.
[0147] The mixture was heated to 50 °C and stirred for 15 hours. The mixture was then heated,
still while stirring, to 80 °C for three hours. The progress of the reactions was
monitored using TLC, by confirming the consumption of the starting materials. The
resulting mixture was poured into water to produce a solid mass of the product compound.
The product was further purified by column chromatography, which yielded a pure, white,
amorphous compound.
Example 8: Calculation of the Instrument Constants A+B
[0148] Three samples of caffeine were subjected to a controlled temperature program as described
in the table below. Each sample weighed approximately 10 mg for the experiment.
| Sample Number |
Temperature |
Hold Time |
Heating Rate |
Vapor Pressure of Caffeine |
| 1 |
Ambient to 170 °C |
-- |
100 °C/min |
|
| |
Hold at 170 °C |
30 minutes |
-- |
64.35 Pa |
| |
Heat to 800 °C |
-- |
50 °C/min |
|
| 2 |
Ambient to 200 °C |
-- |
100 °C/min |
-- |
| |
Hold at 200 °C |
30 minutes |
-- |
453.64 Pa |
| |
Heat to 800 °C |
-- |
50 °C/min |
|
| 3 |
Ambient to 230 °C |
-- |
100 °C/min |
-- |
| |
Hold at 230 °C |
30 minutes |
-- |
3198.06 Pa |
| |
Heat to 800 °C |
-- |
50 °C/min |
|
[0149] The data was then plotted as a function of mass (mg) vs time (minutes). The derivative
of the data during the isothermal hold period was determined for each temperature
and the average value of that region was taken to be the dm/dt value. In order to
determine the a and b constants, a line was fitted through the plot of the natural
log of the dm/dt values versus the natural log of the vapor pressures (see table above).
The a and b values are defined by the linear equation's slope and intercept, respectively.
[0150] Once the a and b values have been determined, they are valid as long as there are
no modifications that would significantly affect the gas flow or temperature distribution
within the furnace or sample pan of the instrument. This calibration will hold over
a larger temperature range than the one used for the calibration.
Example 9: Vapor Pressure
[0151] Instrument calibration was based on samples of known vapor pressure to determine
instrument specific constants a and b from the equation:

[0152] P is the vapor pressure in Pascals (1 atm = 101325 Pa) at temperature T and dm/dt
is the mass loss rate at temperature T. Empty pan data was gathered to determine the
sensitivity range of the instrument as a function of temperature. The values for a
and b were determined to be 1.2394 and 8.8337 respectively. The empty pan data is
summarized in the table below:
| Temperature (°C) |
Intercept (from fit of dm/dt) |
Error |
Maximum P (Pa) |
| 120 |
-1.85E-04 |
1.87E-04 |
0.012969579 |
| 180 |
-1.23E-04 |
2.21E-04 |
0.673526029 |
| 240 |
1.34E-04 |
2.47E-04 |
2.609012695 |
| 280 |
7.69E-06 |
1.89E-04 |
1.349742044 |
[0153] In the table above, the maximum P is determined from the intercept value of the fit
line combined with the error value. In this manner, the positive dm/dt values are
identified and the proper mathematical formula is applied. The vapor pressure values
are very low for the pans and that the range of the fit data would add an uncertainty
of approximately 3 Pa to the results.
[0154] At 260 °C, the XCP series for compounds 1-6 gave the following results, adjusted
for the uncertainty above.
| Compound |
Vapor Pressure at 260 °C (Pa) |
| XCP-1 |
1.84±3 |
| XCP-2 |
2.18±3 |
| XCP-3 |
1.95±3 |
| XCP-4 |
7.83±3 |
| XCP-5 |
0.78±3 |
| XCP-6 |
4.03±3 |
[0155] The vapor pressure of the materials at 260 °C is shown to be essentially zero, i.e.,
they are not volatile. XCP-3 was then tested in the range in which PET is dried and
the following results were obtained compared to PET.
| Sample |
120 °C |
140 °C |
160 °C |
180 °C |
| PET |
0.109±3 |
0.354±3 |
0±3 |
0.024±3 |
| XCP-3 |
0.273±3 |
0.075±3 |
0.056±3 |
0±3 |
[0156] PET is shown to be essentially non-volatile over the period of 20 minutes that it
takes to measure the vapor pressure, but practical experience shows that even over
several hours there is minimal mass loss excluding that of water.
[0157] A measurement at 260 °C that shows low vapor pressure (i.e., less than about 25 Pa),
will ensure that the material can be both processed and dried with PET.
1. A polyester container having enhanced gas barrier properties comprising a polyester
composition comprising a polyester and a gas barrier enhancing additive, wherein the
gas barrier enhancing additive is a compound having the chemical structure of Formula
I:
wherein i, ii, iii, iv, v, n, n', n", n"', and m are 0 or 1;
wherein p is an integer from 0 to 50;
wherein Z is a carbon or nitrogen atom;
wherein A, A', A", A‴, and Ae are selected from the group consisting of hydrogen, hydroxyl, primary amine, secondary
amine, and unsubstituted or substituted C1-C20 hydrocarbyl, wherein the C1-C20 hydrocarbyl is mono-, di-, tri-, or tetravalent;
wherein each Y, independent of one another, comprises a compound having the chemical
structure of Formula II:

wherein t, t1, x, x1, x2, y, and z, independent of one another, are a single bond or a double bond; wherein
t', x', y', and z', independent of one another, are 0 or 1; wherein x", y", and w',
independent of one another, are 0, 1 or 2;
wherein when one or more of ii, iii, iv, and v are 1, A, A' (or Ae), A", and A‴, respectively and independent of one other, is singly or doubly bonded
to atom a, c, or f in structure Y, or singly bonded to atom b, d, e, or g in structure
Y;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom b in structure Y, x' is 0,
and x is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom c in structure Y, y" is 1 and
y is a single bond, or y" is 0 and y is a double bond; wherein when one or more of
A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom c in structure Y, y" is 0 and
y is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom d in structure Y, y' is 0 and
y is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom a in structure Y, x" is 1 and
both x and x1 are single bonds, or x" is 0 and one of x and x1 is a double bond; wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom a in structure Y, x" is 0 and
both x and x1 are single bonds;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom e in structure Y, z' is 0 and
z is a single bond;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom f in structure Y, w' is 1 and
both z and t are single bonds, or w' is 0 and one of z and t is a double bond; wherein
when one or more of A, A', A", A‴, and Ae, independent of one another, is doubly bonded to atom f in structure Y, w' is 0 and
both z and t are single bonds;
wherein when one or more of A, A', A", A‴, and Ae, independent of one another, is singly bonded to atom g in structure Y, t' is 0 and
both t and t1 are single bonds;
wherein when x is a double bond, x1 is a single bond; wherein when x1 is a double bond, x and x2 are single bonds; wherein when x2 is a double bond, x1 and t1 are single bonds; wherein when t is a double bond, t1 and z are single bonds; wherein when z is a double bond, t is a single bond; wherein
when t1 is a double bond, t and x2 are single bonds; wherein when x is a double bond, x' is 0; wherein when x or x1 is a double bond, x" is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom a in structure Y; wherein
when y is a double bond, y' is 0 and y" is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom c in structure Y; wherein
when t or t1 is a double bond, t' is 0; wherein when z and t are single bonds, w' is 2 if one
or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom f in structure Y; wherein
when z or t is a double bond, w' is 1 if one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atom f in structure Y; wherein
when z is a double bond, z' is 0; wherein when x, y, or z, independent of one another,
is a single bond and one or more of A, A', A", A‴, or Ae, independent of one another, is not singly bonded to atoms b, d, or e, respectively,
in structure Y, x', y', or z', independent of one another, is 1;
wherein R1, R3, R5, and R7, independent of one another, comprise a hydrogen, arylamino, alkoxy, aryloxy, alkenyl,
alkynyl, or a straight, chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl,
heteroaryl, heterocyclic, or acyl group;
wherein R2, R4, and R6, independent of one another, may be moieties attached by a single or double bond;
wherein when R2, R4, or R6 is a moiety attached by a single bond, R2, R4, and R6, independent of one another, comprise a hydrogen, hydroxyl, amino, amido, alkylamino,
arylamino, alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato,
mercapto, imino, sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl,
phosphoryl, phosphino, thioester, thioether, anhydride, oximno, hydrazino, carbamyl,
phosphonic acid, phosphonato, or a straight, chained, branched, or cyclic alkyl, alkenyl,
alkynyl, aryl, heteroaryl, heterocyclic, or acyl group;
wherein when R2, R4, or R6 is a moiety attached by a double bond, R2, R4, or R6, independent of one another, comprise oxygen, sulfur, CR8R9, SO2, NR10; wherein R8 and R9, independent of one another, comprise a hydrogen, hydroxyl, amino, amido, alkylamino,
arylamino, alkoxy, aryloxy, nitro, acyl, alkenyl, alkynyl, cyano, sulfo, sulfato,
mercapto, imino, sulfonyl, sulfenyl, sulfinyl, sulfamoyl, phosphonyl, phosphinyl,
phosphoryl, phosphino, thioester, thioether, anhydride, oximno, hydrazino, carbamyl,
phosphonic acid, phosphonato, or a straight, chained, branched, or cyclic alkyl, alkenyl,
alkynyl, aryl, heteroaryl, heterocyclic, or acyl group; and R10 comprises a hydrogen, arylamino, alkoxy, aryloxy, alkenyl, alkynyl, or a straight,
chained, branched, or cyclic alkyl, alkenyl, alkynyl, aryl, heteroaryl, heterocyclic,
or acyl group;
wherein when x" is 2, both R4 moieties may be the same or different; wherein when y" is 2, both R2 moieties may be the same or different; and wherein when w' is 2, both R6 moieties may be the same or different;
and wherein the gas barrier enhancing additive is a purine derivative selected from
the group consisting of purine dimers, purine trimers and purine tetramers.
2. The polyester container of claim 1, wherein the polyester is selected from the group
consisting of PET, PET copolymer. PEN, polyethylene isophthalate, aliphatic polyesters
and combinations thereof.
3. The polyester container of claim 2, wherein the polyester is PET or a PET copolymer.
4. The polyester container of claim 1, wherein the loading level of the gas barrier enhancing
additive is in the range of 0.1 to 40 weight percent of the polyester composition.
5. The polyester container of claim 1, wherein the gas barrier enhancing additive has
a molecular weight greater than 194 g/mole.
6. The polyester container of claim 1, wherein the vapor pressure of the gas barrier
enhancing additive at 260 °C is less than 25 Pa.
7. A method for forming a hollow plastic container comprising:
(i) providing a polyester resin material;
(ii) heating the polyester resin material to provide a molten resin;
(iii) adding a gas barrier enhancing additive as defined in claim 1 to the molten
resin;
(iv) introducing the molten resin into a mold;
(v) cooling the molten resin to form a preform;
(vi) removing the perform from the mold; and
(vi) blow molding the perform to form a hollow plastic container.
8. A method for forming a hollow plastic container comprising:
(i) providing a polyester resin material comprising a polyester and a gas barrier
enhancing additive, wherein the gas barrier additive is as defined in claim 1;
(ii) heating the polyester resin material to provide a molten resin;
(iii) introducing the molten resin into a mold;
(iv) cooling the molten resin to form a preform;
(v) removing the perform from the mold; and
(v) blow molding the perform to form a hollow plastic container.
9. The method of claims 7 or 8, wherein the polyester is PET or a PET copolymer.
10. The method of claim 9, wherein the container is a PET bottle.
11. The polyester container of claim 1, wherein the polyester container comprises a plurality
of layers.
12. The polyester container of claim 1, wherein the vapour pressure of the gas barrier
enhancing additive at 260 °C is 0 Pa.
1. Polyesterbehälter mit verbesserten Gasbarriereeigenschaften, umfassend eine Polyesterzusammensetzung,
die einen Polyester und ein Gasbarriereverbesserungsadditiv umfasst, wobei es sich
bei dem Gasbarriereverbesserungsadditiv um eine Verbindung mit der chemischen Struktur
von Formel I handelt:
wobei i, ii, iii, iv, v, n, n', n", n‴ und m für 0 oder 1 steht;
wobei p für eine ganze Zahl von 0 bis 50 steht;
wobei Z für ein Kohlenstoff- oder Stickstoffatom steht; wobei A, A', A", A‴ und Ae aus der Gruppe bestehend aus Wasserstoff, Hydroxyl, primärem Amin, sekundärem Amin
und substituiertem oder unsubstituiertem C1-C20-Hydrocarbyl ausgewählt ist, wobei das C1-C20-Hydrocarbyl ein-, zwei-, drei- oder vierwertig ist;
wobei Y jeweils unabhängig voneinander eine Verbindung mit der chemischen Struktur
der Formel II umfasst:

wobei t, t1, x, x1, x2 und z unabhängig voneinander für eine Einfachbindung oder eine Doppelbindung stehen;
wobei t', x', y' und z' unabhängig voneinander für 0 oder 1 stehen; wobei x'', y''
w' unabhängig voneinander für 0, 1 oder 2 stehen;
wobei dann, wenn eines oder mehrere von ii, iii, iv und v für 1 stehen, A, A' (oder
Ae), A'' bzw. A‴ unabhängig voneinander einfach oder doppelt an Atom a, c oder f in
Struktur Y oder einfach an Atom b, d, e oder g in Struktur Y gebunden ist;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom b in Struktur Y gebunden ist, x' für 0 steht
und x für eine Einfachbindung steht;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom c in Struktur Y gebunden ist, y" für 1 steht
und y für eine Einfachbindung steht oder y" für 0 steht und y für eine Doppelbindung
steht; wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander doppelt an Atom c in Struktur Y gebunden sind, y" für 0 steht
und y für eine Einfachbindung steht;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom d in Struktur Y gebunden ist, y' für 0 steht
und y für eine Einfachbindung steht;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom a in Struktur Y gebunden ist, x" für 1 steht
und sowohl x als auch x1 für Einfachbindungen stehen oder x" für 0 steht und eines von x und x1 für eine Doppelbindung steht; wobei dann, wenn eines oder mehrere von A, A', A",
A‴ und Ae unabhängig voneinander doppelt an Atom a in Struktur Y gebunden sind, x" für 0 steht
und sowohl x als auch x1 für Einfachbindungen stehen;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom e in Struktur Y gebunden ist, z' für 0 steht
und z für eine Einfachbindung steht;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom f in Struktur Y gebunden ist, w' für 1 steht
und sowohl z als auch t für Einfachbindungen stehen oder w' für 0 steht und eines
von z und t für eine Doppelbindung steht; wobei dann, wenn eines oder mehrere von
A, A', A", A‴ und Ae unabhängig voneinander doppelt an Atom f in Struktur Y gebunden sind, w' für 0 steht
und sowohl z als auch t für Einfachbindungen stehen;
wobei dann, wenn eines oder mehrere von A, A', A", A‴ und Ae unabhängig voneinander einfach an Atom g in Struktur Y gebunden ist, t' für 0 steht
und sowohl t als auch t1 für Einfachbindungen stehen;
wobei dann, wenn x für eine Doppelbindung steht, x1 für eine Einfachbindung steht; wobei dann, wenn x1 für eine Doppelbindung steht, x und x2 für Einfachbindungen stehen; wobei dann, wenn x2 für eine Doppelbindung steht, x1 und t1 für Einfachbindungen stehen; wobei dann, wenn t für eine Doppelbindung steht, t1 und z für Einfachbindungen stehen; wobei dann, wenn z für eine Doppelbindung steht,
t für eine Einfachbindung steht; wobei dann, wenn t1 für eine Doppelbindung steht, t und x2 für Doppelbindungen stehen; wobei dann, wenn x für eine Doppelbindung steht, x' für
0 steht; wobei dann, wenn x oder x1 für eine Doppelbindung steht, x" für 1 steht, falls eines oder mehrere von A, A',
A", A‴ oder Ae unabhängig voneinander nicht einfach an Atom a in Struktur Y gebunden ist; wobei
dann, wenn y für eine Doppelbindung steht, y' für 0 steht und y" für 1 steht, falls
eines oder mehrere von A, A', A", A‴ oder Ae unabhängig voneinander nicht einfach an Atom c in Struktur Y gebunden ist; wobei
dann, wenn t oder t1 für eine Doppelbindung steht, t' für 0 steht; wobei dann, wenn z und t für Einfachbindungen
stehen, w' für 2 steht, falls eines oder mehrere von A, A', A", A‴ ' oder Ae unabhängig voneinander nicht einfach an Atom f in Struktur Y gebunden ist; wobei
dann, wenn z oder t für eine Doppelbindung steht, w' für 1 steht, falls eines oder
mehrere von A, A', A", A‴ oder Ae unabhängig voneinander nicht einfach an Atom f in Struktur Y gebunden ist; wobei
dann, wenn z für eine Doppelbindung steht, z' für 0 steht; wobei dann, wenn x, y oder
z unabhängig voneinander für eine Einfachbindung steht und falls eines oder mehrere
von A, A', A", A‴ oder Ae unabhängig voneinander nicht einfach an Atom b, d bzw. e in Struktur Y gebunden ist,
x', y' oder z' unabhängig voneinander für 1 steht;
wobei R1, R3, R5 und R7 unabhängig voneinander eine Wasserstoff-, Arylamino-, Alkoxy-, Aryloxy-, Alkenyl-,
Alkinyl- oder geradkettige, verzweigte oder cyclische Alkyl-, Alkenyl-, Alkinyl-,
Aryl-, Heteroaryl-, Heterocyclyl- oder Acylgruppe umfassen;
wobei R2, R4 und R6 unabhängig voneinander für Gruppierungen, die über eine einfach- oder Doppelbindung
gebunden sind, stehen können;
wobei dann, wenn R2, R4 oder R6 für eine über eine Einfachbindung gebundene Gruppierung steht, R2, R4 und R6 unabhängig voneinander eine Wasserstoff-, Hydroxyl-, Amino-, Amido-, Alkylamino-,
Arylamino-, Alkoxy-, Aryloxy-, Nitro-, Acyl-, Alkenyl-, Alkinyl-, Cyano-, Sulfo-,
Sulfato-, Mercapto-, Imino-, Sulfonyl-, Sulfenyl-, Sulfinyl-, Sulfamoyl-, Phosphonyl-,
Phosphinyl-, Phosphoryl-, Phosphino-, Thioester-, Thioether-, Anhydrid-, Oximo-, Hydrazino-,
Carbamyl-, Phosphonsäure-, Phosphonato- oder geradkettige, verzweigte oder cyclische
Alkyl-, Alkenyl-, Alkinyl-, Aryl-, Heteroaryl-, Heterocyclyl- oder Acylgruppe umfassen;
wobei dann, wenn R2, R4 oder R6 für eine über eine Doppelbindung gebundene Gruppierung steht, R2, R4 und R6 unabhängig voneinander Sauerstoff, Schwefel, CR8R9, SO2, NR10 umfassen; wobei R8 und R9 unabhängig voneinander eine Wasserstoff-, Hydroxyl-, Amino-, Amido-, Alkylamino-,
Arylamino-, Alkoxy-, Aryloxy-, Nitro-, Acyl-, Alkenyl-, Alkinyl-, Cyano-, Sulfo-,
Sulfato-, Mercapto-, Imino-, Sulfonyl-, Sulfenyl-, Sulfinyl-, Sulfamoyl-, Phosphonyl-,
Phosphinyl-, Phosphoryl-, Phosphino-, Thioester-, Thioether-, Anhydrid-, Oximo-, Hydrazino-,
Carbamyl-, Phosphonsäure-, Phosphonato- oder geradkettige, verzweigte oder cyclische
Alkyl-, Alkenyl-, Alkinyl-, Aryl-, Heteroaryl-, Heterocyclyl- oder Acylgruppe umfassen
und R10 eine Wasserstoff-, Arylamino-, Alkoxy-, Aryloxy-, Alkenyl-, Alkinyl- oder geradkettige,
verzweigte oder cyclische Alkyl-, Alkenyl-, Alkinyl-, Aryl-, Heteroaryl-, Heterocyclyl-
oder Acylgruppe umfasst;
wobei dann, wenn x" für 2 steht, die beiden R4-Gruppierungen gleich oder verschieden sein können; wobei dann, wenn y" für 2 steht,
die beiden R2-Gruppierungen gleich oder verschieden sein können; und wobei dann, wenn w' für 2
steht, die beiden R6-Gruppierungen gleich oder verschieden sein können;
und wobei es sich bei dem Gasbarriereverbesserungsadditiv um ein Purinderivat aus
der Gruppe bestehend aus Purindimeren, Purintrimeren und Purintetrameren handelt.
2. Polyesterbehälter nach Anspruch 1, wobei der Polyester aus der Gruppe bestehend aus
PET, PET-Copolymer, PEN, Polyethylenisophthalat, aliphatischen Polyestern und Kombinationen
davon ausgewählt ist.
3. Polyesterbehälter nach Anspruch 2, wobei es sich bei dem Polyester um PET oder PET-Copolymer
handelt.
4. Polyesterbehälter nach Anspruch 1, wobei das Beladungsniveau des Gasbarriereverbesserungsadditivs
im Bereich von 0,1 bis 40 Gewichtsprozent der Polyesterzusammensetzung liegt.
5. Polyesterbehälter nach Anspruch 1, wobei das Gasbarriereverbesserungsadditiv ein Molekulargewicht
von mehr als 194 g/mol aufweist.
6. Polyesterbehälter nach Anspruch 1, wobei der Dampfdruck des Gasbarriereverbesserungsadditivs
bei 260 °C weniger als 25 Pa beträgt.
7. Verfahren zum Bilden eines hohlen Kunststoffbehälters, das Folgendes umfasst:
(i) Bereitstellen eines Polyesterharzmaterials;
(ii) Erhitzen des Polyesterharzmaterials zum Bereitstellen eines geschmolzenen Harzes;
(iii) Zugeben eines Gasbarriereverbesserungsadditivs gemäß Anspruch 1 zu dem geschmolzenen
Harz;
(iv) Eintragen des geschmolzenen Harzes in eine Form;
(v) Abkühlen des geschmolzenen Harzes zur Bildung eines Vorformlings;
(vi) Herausnehmen des Vorformlings aus der Form; und
(vi) Blasformen des Vorformlings zur Bildung eines hohlen Kunststoffbehälters.
8. Verfahren zum Bilden eines hohlen Kunststoffbehälters, das Folgendes umfasst:
(i) Bereitstellen eines Polyesterharzmaterials, das einen Polyester und ein Gasbarriereverbesserungsadditiv
umfasst, wobei das Gasbarriereadditiv wie in Anspruch 1 definiert ist;
(ii) Erhitzen des Polyesterharzmaterials zum Bereitstellen eines geschmolzenen Harzes;
(iii) Eintragen des geschmolzenen Harzes in eine Form;
(iv) Abkühlen des geschmolzenen Harzes zur Bildung eines Vorformlings;
(v) Herausnehmen des Vorformlings aus der Form; und
(v) Blasformen des Vorformlings zur Bildung eines hohlen Kunststoffbehälters.
9. Verfahren nach Anspruch 7 oder 8, wobei es sich bei dem Polyester um PET oder PET-Copolymer
handelt.
10. Verfahren nach Anspruch 9, wobei es sich bei dem Behälter um eine PET-Flasche handelt.
11. Polyesterbehälter nach Anspruch 1, wobei der Polyesterbehälter mehrere Schichten umfasst.
12. Polyesterbehälter nach Anspruch 1, wobei der Dampfdruck des Gasbarriereverbesserungsadditivs
bei 260 °C 0 Pa beträgt.
1. Récipient de polyester possédant des propriétés de barrière aux gaz améliorées comprenant
une composition de polyester comprenant un polyester et un additif d'amélioration
de la barrière aux gaz, l'additif d'amélioration de la barrière aux gaz étant un composé
possédant la structure chimique de formule I :
i, ii, iii, iv, v, n, n', n", n‴, et m étant 0 ou 1 ;
p étant un entier de 0 à 50 ;
Z étant un atome de carbone ou d'azote ;
A, A', A", A‴, et Ae étant choisis dans le groupe constitué par hydrogène, hydroxyle, amine primaire,
amine secondaire, et C1-C20 hydrocarbyle non substitué ou substitué, le C1-C20 hydrocarbyle étant monovalent, divalent, trivalent ou tétravalent ;
chaque Y, indépendamment les uns des autres, comprenant un composé possédant la structure
chimique de formule II :

t, t1, x, x1, x2, y, et z, indépendamment les uns des autres, étant une simple liaison ou une double
liaison ; t', x', y', et z', indépendamment les uns des autres, étant 0 ou 1 ; x",
y", et w', indépendamment les uns des autres, étant 0, 1 ou 2 ; dans laquelle lorsque
l'un ou plusieurs parmi ii, iii, iv, et v sont 1, A, A' (ou Ae), A", et A'", respectivement et indépendamment les uns des autres, sont liés simplement
ou doublement à l'atome a, c, ou f dans la structure Y, ou liés simplement à l'atome
b, d, e, ou g dans la structure Y ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome b dans la structure
Y, x' est 0, et x est une simple liaison ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome c dans la structure
Y, y" est 1 et y est une simple liaison, ou y" est 0 et y est une double liaison ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont doublement liés à l'atome c dans la structure
Y, y" est 0 et y est une simple liaison ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome d dans la structure
Y, y' est 0 et y est une simple liaison ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome a dans la structure
Y, x" est 1 et à la fois x et x1 sont des simples liaisons, ou x" est 0 et l'un parmi x et x1 est une double liaison ; dans laquelle lorsque l'un ou plusieurs parmi A, A', A",
A‴, et Ae, indépendamment les uns des autres, sont doublement liés à l'atome a dans la structure
Y, x" est 0 et à la fois x et x1 sont des simples liaisons ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome e dans la structure
Y, z' est 0 et z est une simple liaison ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome f dans la structure
Y, w' est 1 et à la fois z et t sont des simples liaisons, ou w' est 0 et l'un parmi
z et t est une double liaison ; dans laquelle lorsque l'un ou plusieurs parmi A, A',
A", A‴, et Ae, indépendamment les uns des autres, sont doublement liés à l'atome f dans la structure
Y, w' est 0 et à la fois z et t sont des simples liaisons ;
dans laquelle lorsque l'un ou plusieurs parmi A, A', A", A‴, et Ae, indépendamment les uns des autres, sont liés simplement à l'atome g dans la structure
Y, t' est 0 et à la fois t et t1 sont des simples liaisons ;
dans laquelle lorsque x est une double liaison, x1 est une simple liaison ; dans laquelle lorsque x1 est une double liaison, x et x2 sont des simples liaisons ; dans laquelle lorsque x2 est une double liaison, x1 et t1 sont des simples liaisons ; dans laquelle lorsque t est une double liaison, t1 et z sont des simples liaisons ; dans laquelle lorsque z est une double liaison,
t est une simple liaison ;
dans laquelle lorsque t1 est une double liaison, t et x2 sont des simples liaisons ; dans laquelle lorsque x est une double liaison, x' est
0 ; dans laquelle lorsque x ou x1 est une double liaison, x" est 1 si l'un ou plusieurs parmi A, A', A", A‴, ou Ae, indépendamment les uns des autres, ne sont pas liés simplement à l'atome a dans
la structure Y ; dans laquelle lorsque y est une double liaison, y' est 0 et y" est
1 si l'un ou plusieurs parmi A, A', A", A‴, ou Ae, indépendamment les uns des autres, ne sont pas liés simplement à l'atome c dans
la structure Y ; dans laquelle lorsque t ou t1 est une double liaison, t' est 0 ; dans laquelle lorsque z et t sont des simples
liaisons, w' est 2 si l'un ou plusieurs parmi A, A', A", A‴, ou Ae, indépendamment les uns des autres, ne sont pas liés simplement à l'atome f dans
la structure Y ; dans laquelle lorsque z ou t est une double liaison, w' est 1 si
l'un ou plusieurs parmi A, A', A", A‴, ou Ae, indépendamment les uns des autres, ne sont pas liés simplement à l'atome f dans
la structure Y ; dans laquelle lorsque z est une double liaison, z' est 0 ; dans laquelle
lorsque x, y, ou z, indépendamment les uns des autres, est une simple liaison et l'un
ou plusieurs parmi A, A', A", A‴, ou Ae, indépendamment les uns des autres, ne sont pas liés simplement à l'atome b, d, ou
e, respectivement, dans la structure Y, x', y', ou z', indépendamment les uns des
autres, est 1 ;
R1, R3, R5, et R7, indépendamment les uns des autres, comprenant un hydrogène, arylamino, alcoxy, aryloxy,
alcényle, alcynyle, ou un groupe alkyle linéaire, caténaire, ramifié ou cyclique,
alcényle, alcynyle, aryle, hétéroaryle, hétérocyclique, ou acyle ;
R2, R4, et R6, indépendamment les uns des autres, pouvant être des groupements fixés par une simple
liaison ou une double liaison ;
dans laquelle lorsque R2, R4, ou R6 est un groupement fixé par une simple liaison, R2, R4, et R6, indépendamment les uns des autres, comprennent un groupe hydrogène, hydroxyle, amino,
amido, alkylamino, arylamino, alcoxy, aryloxy, nitro, acyle, alcényle, alcynyle, cyano,
sulfo, sulfato, mercapto, imino, sulfonyle, sulfényle, sulfinyle, sulfamoyle, phosphonyle,
phosphinyle, phosphoryle, phosphino, thioester, thioéther, anhydride, oximno, hydrazino,
carbamyle, acide phosphonique, phosphonato, ou un groupe alkyle linéaire, caténaire,
ramifié ou cyclique, alcényle, alcynyle, aryle, hétéroaryle, hétérocyclique, ou acyle
; dans laquelle lorsque R2, R4, ou R6 est un groupement fixé par une double liaison, R2, R4, ou R6, indépendamment les uns des autres, comprend oxygène, soufre, CR8R9, SO2, NR10 ; dans laquelle R8 et R9, indépendamment les uns des autres, comprenant un groupe hydrogène, hydroxyle, amino,
amido, alkylamino, arylamino, alcoxy, aryloxy, nitro, acyle, alcényle, alcynyle, cyano,
sulfo, sulfato, mercapto, imino, sulfonyle, sulfényle, sulfinyle, sulfamoyle, phosphonyle,
phosphinyle, phosphoryle, phosphino, thioester, thioéther, anhydride, oximno, hydrazino,
carbamyle, acide phosphonique, phosphonato, ou un groupe alkyle linéaire, caténaire,
ramifié ou cyclique, alcényle, alcynyle, aryle, hétéroaryle, hétérocyclique, ou acyle
; et R comprend un groupe hydrogène, arylamino, alcoxy, aryloxy, alcényle, alcynyle,
ou un groupe alkyle linéaire, caténaire, ramifié ou cyclique, alcényle, alcynyle,
aryle, hétéroaryle, hétérocyclique, ou acyle ;
dans laquelle lorsque x" est 2, les deux groupements R4 peuvent être identiques ou différents ; dans laquelle lorsque y" est 2, les deux
groupements R2 peuvent être identiques ou différents ; et dans laquelle lorsque w' est 2, les deux
groupements R6 peuvent être identiques ou différents ;
et l'additif d'amélioration de la barrière aux gaz étant un dérivé de purine choisi
dans le groupe constitué par des dimères de purine, des trimères de purine et des
tétramères de purine.
2. Récipient de polyester selon la revendication 1, le polyester étant choisi dans le
groupe constitué par un PET, un copolymère de PET, un PEN, un poly(isophtalate d'éthylène),
des polyesters aliphatiques et des combinaisons correspondantes.
3. Récipient de polyester selon la revendication 2, le polyester étant un PET ou un copolymère
de PET.
4. Récipient de polyester selon la revendication 1, le taux de charge de l'additif d'amélioration
de la barrière aux gaz étant dans la plage de 0,1 à 40 pour cent en poids de la composition
de polyester.
5. Récipient de polyester selon la revendication 1, l'additif d'amélioration de la barrière
aux gaz possédant un poids moléculaire supérieur à 194 g/mole.
6. Récipient de polyester selon la revendication 1, la pression de vapeur de l'additif
d'amélioration de la barrière aux gaz à 260 °C étant inférieure à 25 Pa.
7. Procédé pour la formation d'un récipient creux en matière plastique comprenant :
(i) la mise à disposition d'un matériau de résine de polyester ;
(ii) le chauffage du matériau de résine de polyester pour fournir une résine fondue
;
(iii) l'ajout d'un additif d'amélioration de la barrière aux gaz tel que défini dans
la revendication 1 à la résine fondue ;
(iv) l'introduction de la résine fondue dans un moule ;
(v) le refroidissement de la résine fondue pour former une préforme ;
(vi) le retrait de la préforme du moule ; et
(vii) le moulage par soufflage de la préforme pour former un récipient creux en matière
plastique.
8. Procédé pour la formation d'un récipient creux en matière plastique comprenant :
(i) la mise à disposition d'un matériau de résine de polyester comprenant un polyester
et un additif d'amélioration de la barrière aux gaz, l'additif de barrière aux gaz
étant tel que défini dans la revendication 1 ;
(ii) le chauffage du matériau de résine de polyester pour fournir une résine fondue
;
(iii) l'introduction de la résine fondue dans un moule ;
(iv) le refroidissement de la résine fondue pour former une préforme ;
(v) le retrait de la préforme du moule ; et
(vi) le moulage par soufflage de la préforme pour former un récipient creux en matière
plastique.
9. Procédé selon les revendications 7 ou 8, le polyester étant un PET ou un copolymère
de PET.
10. Procédé selon la revendication 9, le récipient étant une bouteille en PET.
11. Récipient de polyester selon la revendication 1, le récipient de polyester comprenant
une pluralité de couches.
12. Récipient de polyester selon la revendication 1, la pression de vapeur de l'additif
d'amélioration de la barrière aux gaz à 260 °C étant de 0 Pa.